An extension of CEOS/AE zero-pressure mixing rules for an optimum two-parameter cubic equation of state

Industrial and Engineering Chemistry Research

Volumn 41, Issue 5, 2002, Pages 931-937

  Twu, Chorng H ^a   Sim, Wayne D ^b   Tassone, Vince ^b  

^a Hyprotech Ltd   (United States)

^b NONE   (Canada)

Author keywords

[No Author keywords available]

Indexed keywords

HYDROCARBONS; PETROLEUM REFINERIES; PETROLEUM RESERVOIRS; PHASE EQUILIBRIA;

MIXING RULES;

EQUATIONS OF STATE;

HYDROCARBON;

EQUATION OF STATE; MIXING RULE;

ARTICLE; CHEMICAL COMPOSITION; DENSITY; FLUID TRANSPORT; MATHEMATICAL ANALYSIS; MATHEMATICAL PARAMETERS; PREDICTION; PRESSURE;

EID: 0037028809     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie0101588     Document Type: Article

References (13)

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5. Connection between zero-pressure mixing rules and infinite-pressure mixing rules
6. Comparison of the Peng-Robinson and Soave-Redlich-Kwong equations of state using a new zero-pressure-based mixing rule for the prediction of high-pressure and high-temperature phase equilibria
7. A zero-pressure cubic equation of state mixing rule for predicting high-pressure phase equilibria using infinite dilution activity coefficients at low temperature
8. A new cubic equation of state
9. A modified van der Waals type equation of state
10. 2 phase equilibria
11. A cubic equation of state with a new alpha function and a new mixing rule
12. A modified Trebble-Bishnoi equation of state: Thermodynamic consistency revisited